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MANIPULATION OF AMYLASE REACTION TO IMPROVE THE REDUCING SUGARS PRODUCTION CHAN CHIA SING UNIVERSITI TEKNOLOGI MALAYSIA

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  • MANIPULATION OF AMYLASE REACTION TO IMPROVE THE REDUCING

    SUGARS PRODUCTION

    CHAN CHIA SING

    UNIVERSITI TEKNOLOGI MALAYSIA

    PDF processed with CutePDF evaluation edition www.CutePDF.comPDF processed with CutePDF evaluation edition www.CutePDF.com

  • MANIPULATION OF AMYLASE REACTION TO IMPROVE THE REDUCING

    SUGARS PRODUCTION

    CHAN CHIA SING

    A dissertation submitted in partial fulfilment of the

    requirements for the award of the degree of

    Master of Science (Biotechnology)

    Faculty of Biosciences and Bioengineering

    Universiti Teknologi Malaysia

    JULY 2012

  • iii

    To my beloved family

  • iv

    ACKNOWLEDGEMENT

    This dissertation would not have been possible without the guidance and help

    of several individuals who in one way or another contributed and extended their

    valuable assistance in the preparation and completion of this study. In particular, I

    wish to express my sincere appreciation to my main supervisor, Dr. Goh Kian Mau,

    for encouragement, guidance and critics throughout the whole research. He also gave

    me the opportunity to study and providing me with the greatest stimulus for this

    research topic. Without his continued support, this dissertation would not have been

    the same as presented here.

    Secondary, I would like to give my special appreciation to my dearest family

    who support me with lots of concern and encouragement, so that I can complete this

    project successfully. Their supports provide me the spirit to cope the obstacles.

    Next, I would like to thank to all my friends and my laboratory colleagues for

    their understanding, support and encouragements when I was facing the difficulty to

    carry out the project. Special thanks to Ummirul Mukminin, Chai Yen Yen, Ranjani

    Velayudhan and Chai Kian Piaw who had provided assistance at various occasions

    and guided me continuously until completing this project. Their views and tips are

    useful indeed.

    Last but not least, I would like to thank to all the lab assistants for their

    willingness to assist me and provide me with every kinds of services during the

    dissertation preparation. Unfortunately, it is not possible to list all of them in this

    limited space. I am grateful to all the people that I contacted with.

  • v

    ABSTRACT

    An Anoxybacillus strain SK3-4 was previously isolated from Perak Sungai

    Klah hot spring. The α-amylase gene fragment from Anoxybacillus sp. denoted as

    ASKA was cloned into pET-22b(+) and transformed into Escherichia coli BL21

    (DE3). However, the reactivity and productivity of this amylase is underexplored.

    The main objective of this project is to optimize the reducing sugars production using

    Response Surface Methodology (RSM). The ASKA substrate specificity was

    determined using soluble starch and nine different commercial starches: corn,

    tapioca, wheat, potato, rice, sago, rye, green peas and glutinous rice starch. Sago

    starch was found to be the best substrate with highest reducing sugars production.

    Variable parameters such as reaction temperature, sago starch and ASKA

    concentration were screened using one-factor-at-a-time (OFAT) approach before

    they were optimized through two-level full factorial design and central composite

    rotatable design (CCRD). Statistical analysis showed that all the three parameters

    were significant factors in 23 full factorial design before further optimized the

    reducing sugars production with CCRD. The final optimized parameters using

    CCRD was capable to produce 7.97 g/L reducing sugars with 2.64 % (w/v) sago

    starch and 0.375 unit ASKA under 66.9 ºC reaction temperature. The hydrolysis

    products were determined using High Performance Liquid Chromatography (HPLC).

    Maltose was the major hydrolysis product and no glucose production was detected.

    As a conclusion, applying experimental designs method was able to improve the

    efficiency of reducing sugars production for 87.09 % compared with the reference

    reaction condition with maltose as the major end product.

  • vi

    ABSTRAK

    Satu bakteria species Anoxybacillus (SK3-4) telah berjaya dipencilkan dari

    kolam air panas Sungai Klah (SK) di Perak. Species Anoxybacillus tersebut

    mengandungi gen α-amilase yang di namakan sebagai ASKA. Gen α-amilase itu

    telah diklonkan dalam vektor pET-22b(+) di dalam E. coli BL21 (DE3). Namun

    begitu, tindak balas dan produktiviti α-amilase tersebut masih belum dikaji. Oleh

    yang demikian, objektif utama kajian ini adalah untuk mengoptimumkan penghasilan

    oligosakarida dengan menggunakan Response Surface Methodology (RSM).

    Spesifisiti ASKA terhadap substrat telah ditentukan dengan menggunakan kanji

    terlarut dan sembilan jenis kanji komersil lain iaitu kanji jagung, ubi kayu, gandum,

    kentang, beras, sagu, rai, kacang hijau dan beras pulut. Kanji sagu dikenal pasti

    sebagai substrat terbaik dengan penghasilan oligosakarida tertinggi. Tiga jenis faktor

    iaitu suhu tindak balas, kepekatan kanji sagu dan kepekatan ASKA telah disaring

    dengan menggunakan kaedah satu-faktor-pada-satu masa (OFAT). Analisis

    statistikal rekabentuk 2k faktorial penuh menunjukkan bahawa ketiga-tiga faktor itu

    adalah signifikan dalam mempengaruhi penghasilan oligosakarida. Ketiga-tiga faktor

    itu kemudian dimanipulasi menggunakan rekabentuk komposit kebolehputaran pusat

    (CCRD) untuk mengoptimumkan penghasilan oligosakarida. Keadaan tindak balas

    yang optimum adalah pada suhu 66.9 ºC, 2.64 % (w/v) kanji sagu dan 0.375 unit

    ASKA dengan penghasilan oligosakarida sebanyak 7.97 g/L. High Performance

    Liquid Chromatography (HPLC) kemudiannya digunakan bagi menentukan produk

    hidrolisis itu. Maltosa adalah produk utama hidrolisis dan tiada penghasilan glukosa

    dicatat. Kesimpulannya, penggunaan rekabentuk eksperimen berjaya meningkatkan

    penghasilan oligosakarida sebanyak 87.09 % daripada tindak balas rujukan dengan

    maltosa sebagai produk utama hidrolisis.

  • vii

    TABLE OF CONTENTS

    CHAPTER TITLE PAGE

    TITLE i

    DECLARATION ii

    DEDICATION iii

    ACKNOWLEDGEMENTS iv

    ABSTRACT v

    ABSTRAK vi

    TABLE OF CONTENTS vii

    LIST OF TABLES xi

    LIST OF FIGURES xiii

    LIST OF ABBREVIATIONS xv

    LIST OF APPENDICES xviii

    1 INTRODUCTION 1

    1.1 Background of research 1

    1.2 Problem statement 3

    1.3 Objectives 3

    1.4 Scopes of research 3

    2 LITERATURE REVIEW 4

    2.1 Starch 4

    2.2 Amylase 5

    2.3 Alpha-amylase 6

  • viii

    2.4 Factors influencing the hydrolysis reaction 7

    2.4.1 Starch source 8

    2.4.2 Starch concentration 8

    2.4.3 Starch pretreatment property 9

    2.4.4 Source of amylase 9

    2.4.5 Enzyme concentration 10

    2.4.6 Reaction temperature 10

    2.4.7 pH of reaction medium 11

    2.4.8 Effect of additives 11

    2.5 Industrial application of amylases 12

    2.5.1 Alcohol 12

    2.5.2 Baking 13

    2.5.3 High fructose syrup 13

    2.6 Experimental design 14

    2.6.1 Factorial design model (FDM) 15

    2.6.2 Response surface methodology (RSM) 16

    3 MATERIALS AND METHODS 17

    3.1 Bacterial strain 17

    3.2 Chemicals 17

    3.3 General experimental design 18

    3.4 Medium preparation 20

    3.4.1 Luria-Bertani (LB) medium with ampicillin 20

    3.4.2 Dinitrosalicylic acid (DNS) reagent 20

    3.5 Bacterial stock preparation 21

    3.6 α-Amylase expression and concentration 22

    3.6.1 Expression of recombinant α-amylase

    (ASKA)

    22

    3.6.2 Concentration of crude α-amylase 22

    3.6.3 Amylase activity assay 23

    3.7 α-Amylase substrate specificity determination 23

  • ix

    3.8 Variable parameters screening using one-factor-at-a-

    time (OFAT) approach

    24

    3.8.1 Starch concentration 24

    3.8.2 α-Amylase concentration 24

    3.8.3 Calcium chloride (CaCl2) concentration 25

    3.8.4 Incubation temperature 25

    3.9 Experimental design 26

    3.9.1 Two-level-factorial design 26

    3.9.2 Central composite rotatable design (CCRD) 28

    3.9.3 Model validation 28

    3.9.4 Analysis of hydrolysis products by HPLC 30

    4 RESULTS AND DISCUSSION 31

    4.1 α-Amylase substrate specificity determination 31

    4.2 Variable parameters screening using one-factor-at-a-

    time (OFAT) approach

    34

    4.2.1 Sago starch concentration 34

    4.2.2 α-Amylase concentration 35

    4.2.3 Calcium chloride (CaCl2) concentration 36

    4.2.4 Reaction temperature 37

    4.3 Optimization of variable parameters using Design of

    Experiment

    37

    4.3.1 23 full factorial design 37

    4.3.2 Central composite rotatable design (CCRD) 43

    4.3.3 Model validation 47

    4.3.4 Interaction among the variables 48

    4.3.5 Model verification 54

    4.4 Analysis of hydrolysis products by HPLC 55

    4.4.1 Analysis of hydrolysis products in different

    time interval by HPLC

    56

  • x

    5 CONCLUSION 58

    5.1 Conclusion 58

    5.2 Future work 59

    RERERENCES 61

    APPENDICES 68

  • xi

    LIST OF TABLES

    TABLE NO. TITLE PAGE

    2.1 α-Amylase family members and their origin (Kuriki

    and Imanaka, 1999)

    7

    3.1 Composition of LB medium per liter 20

    3.2 Composition of 1.0 % (w/v) DNS reagent per liter 21

    3.3 The actual and coded values of each parameter for 23

    factorial design

    27

    3.4 The experimental plan for 23 factorial design in

    actual and coded values. Values in the parenthesis

    indicate the coded values

    27

    3.5 The actual and coded values of each parameter for

    CCRD

    28

    3.6 The experimental plan for CCRD in actual and coded

    values. Values in the parenthesis indicate the coded

    values

    29

    4.1 The reducing sugars production for each substrate at

    12th hour

    34

    4.2 The actual and coded values of each parameter for 23

    factorial design

    38

    4.3 The experimental values and predicted values for 23

    factorial design. Values in the parenthesis indicate

    the coded values

    41

    4.4 Analysis of Variance (ANOVA) for 23 full factorial

    design

    42

    4.5 The actual and coded values of each parameter for

    CCRD

    43

  • xii

    4.6 The experimental values and predicted values for

    CCRD. Values in the parenthesis indicate the coded

    values

    45

    4.7 Analysis of Variance (ANOVA) for CCRD 46

    4.8 Summary of optimum condition for each parameter

    in each model design. Actual value indicates the

    experimental results while predicted value indicates

    the calculated response generated by the model

    55

  • xiii

    LIST OF FIGURES

    FIGURE NO. TITLE PAGE

    2.1 The structures of α-amylose and amylopectin (Stenesh,

    1998)

    5

    3.1 The project overall experimental flow 19

    4.1 The 24-hour-time plot of reducing sugars production for

    ten different starches. (a) Soluble starch; (b) Tapioca

    starch; (c) Potato starch; (d) Wheat starch; (e) Sago

    starch; (f) Rice starch; (g) Green peas starch; (h)

    Glutinous rice starch; (i) Corn starch; (j) Rye starch

    32

    4.2 Reducing sugars production for different sago starch

    concentration

    35

    4.3 Reducing sugars production for different ASKA

    concentration

    36

    4.4 Reducing sugars production for different CaCl2

    concentration

    36

    4.5 Reducing sugars production for different reaction

    temperature

    37

    4.6 Ramp of optimized parameters through 23 full factorial

    design

    40

    4.7 Ramp of optimized parameters through CCRD 44

    4.8 Diagnostic plots for CCRD. (a) Normal plot of residual;

    (b) Plot of residuals versus predicted; (c) Outlier T plot;

    (d) Box-Cox plot

    48

    4.9 Contour and response surface plots for the effect of sago

    starch (% (w/v)) and ASKA concentration (unit)

    towards reducing sugars production

    51

  • xiv

    4.10 Contour and response surface plots for the effect of sago

    starch concentration (% (w/v)) and temperature (ºC)

    towards reducing sugars production

    52

    4.11 Contour and response surface plots for the effect of

    ASKA concentration (unit) and temperature (ºC)

    towards reducing sugars production

    53

    4.12 Production of reducing sugars by various reaction

    conditions

    56

    4.13 Production of reducing sugars at various time intervals 57

    4.14 Reducing sugars production fraction at various time

    intervals

    57

  • xv

    LIST OF SYMBOLS/ ABBREVIATIONS

    ANOVA - Analysis of variance

    ASKA - Anoxybacillus species SK3-4 alpha-amylase

    B. - Bacillus

    Ca2+ - calcium ion

    CaCl2 - calcium chloride

    CCRD - central composite rotatable design

    C.I. - confidence interval

    CV - coefficient of variation

    DNS - 3,5-dinitrosalicylic acid

    E. coli - Escherichia coli

    g - gram

    G1 - glucose

    G2 - maltose

    G3 - maltotriose

    G4 - maltotetraose

    G5 - maltopentaose

    g/L - gram per liter

    HCl - hydrochloric acid

    HPLC - High Performance Liquid Chromatography

    IPTG - isopropyl β-D-thiogalactopyranoside

    IU - international unit

    kDa - kilodalton

    kPa - kilo pascal

    L - liter

    LB - Luria-Bertani

    mg - miligram

  • xvi

    min - minute(s)

    mL - mililiter

    mm - milimeter

    mM - milimolar

    MW - molecular weight

    MWCO - molecular weight cut-off

    NaCl - sodium chloride

    NaOH - sodium hydroxide

    nm - nanometer

    OD - optical density

    OD600 - optical density at 600 nm

    OFAT - one-factor-at-a-time

    PES - polyethersulfone

    PRESS - predicted residual sum of squares

    P-value - probability value

    R2 - coefficient of determination

    rpm - revolutions per minute

    RSM - Response Surface Methodology

    SK - Sungai Klah

    sp. - species

    Tris - tris(hydroxymethyl)methylamine

    U - unit of enzyme activity

    v/v - Volume per volume

    w/v - weight per volume

    α - alpha

    µ - micro

    µg - microgram

    µL - microliter

    µm - micrometer

    µmol - micromole

    % - percentage

    ºC - degree Celcius

    3D - three-dimensional

  • xvii

    LIST OF APPENDICES

    APPENDIX TITLE PAGE

    A List of Medium Preparation 68

    B Determination of α-Amylase Activity Using DNS

    Assay

    69

    C HPLC Standard Curves for Reducing Sugars 70

    D HPLC chromatogram of various reducing sugars

    standards and their retention time

    73

    E HPLC chromatogram of reducing sugars produced

    by various reaction conditions

    74

  • CHAPTER 1

    INTRODUCTION 1.1 Background of research

    Starch is one of the most abundant natural storage polysaccharides

    synthesized by plants. The hydrolysis of the complex starch structure required

    amylolytic enzymes to depolymerise it and form oligosaccharides and small sugars.

    The world today shows an increasing interest in investigating the usage of amylolytic

    enzymes for biorefinery in varieties of industries; include the food product and non-

    food product industries. Amylolytic enzymes act on starch and can be categorized

    into four different groups, i.e. the exo acting amylases, endo acting amylases,

    debranching amylases and cyclodextrinases (Nigam and Pandey, 2009). α-Amylase

    (EC 3.2.1.1) is one of the endo acting amylases (endo-1,4-α-D-glucan

    glucohydrolase) which is capable to hydrolyze internal α-D-1,4-glycosidic linkages

    in amylopectin and glycogen (Richardson et al., 2002).

    Alpha-amylase can be found in plants, animals and microorganisms as it

    plays a dominant role in their carbohydrate metabolism. Since 1980, mesophile

    Bacillus licheniformis (Richardson et al., 2002) is highly used for industrial

    application due to its extreme thermostability. Others α-amylase producers include B.

    subtilis (Konsula and Liakopoulou-Kyriakides, 2003), B. amyloliquefaciens

    (Demirkan, 2005), B. stearothermophilus (Kim et al., 1989), Aspergillus species and

    Penicillium sp. (Gouda and Elbahloul, 2008). Thermophilic Anoxybacillus which

    was first described by Pikuta et al. (2000) also contains the ability to undergo extra-

    cellular amylase activity (Poli et al., 2006).

  • 2

    Amylases have been applied in varieties of industries; include food, textile,

    paper, pharmaceutical and detergent industries (Shigechi et al., 2004). High demand

    of amylases has encouraged the discovery of new amylases from different

    microorganisms sources with an aim to find alternative that could lower the cost and

    power requirement. Amylase reaction condition is also playing an important role for

    enzyme stabilizing, which will subsequently increase the enzyme reactivity and

    influence the products formation (Sivaramakrishnan et al., 2006).

    An in-house Anoxybacillus strain SK3-4 was previously isolated from Sungai

    Klah (Perak) hot spring. The α-amylase gene fragment from Anoxybacillus sp. was

    cloned into pET-22b(+) and transformed into E. coli BL21 (DE3) (Chai, 2012). The

    recombinant α-amylase (denoted as ASKA) has an optimum activity of pH 8 and 60

    °C.

    Physical and chemical parameters are two categories that influence the

    enzymatic hydrolysis reaction (Agrawal et al., 2005). The physical parameters

    include starch source, starch condition, pH of the reaction mixture, reaction

    temperature and the incubation period for enzymatic reaction. While chemical

    parameters are starch concentration, enzyme concentration, presence and the

    concentration of divalent ions and other stabilizing agents (Richardson et al., 2002;

    Sivaramakrishnan et al., 2006; Tester et al., 2006; Tamilarasan et al., 2010).

    Conventional one-factor-at-a-time approach for optimization process is time

    consuming and tedious. Therefore, response surface methodology (RSM) which

    designs and analyzes the experimental result through mathematical and statistical

    techniques can be useful to solve the complexity of one-factor-at-a-time approach

    and optimize the response. In this study, two-level-full-factorial and central

    composite design (CCD) will be applied to optimize the reducing sugars production

    which involves various factors such as reaction temperature, starch and α-amylase

    concentration.

  • 3

    1.2 Problem statement

    The study of amylase from Anoxybacillus is an interesting field since the

    function and reactivity of this amylase is underexplored. The application of ASKA is

    an economic alternative for high temperature liquefaction process. Thus, optimize

    the reducing sugars production by novel recombinant amylase is important. This

    ultimately provides an alternative to produce high amount of reducing sugars with

    less expenditures.

    1.3 Objectives

    i. To identify the best substrate for Anoxybacillus sp. amylase (ASKA).

    ii. To screen the variable parameters that will influence the reducing sugars

    production.

    iii. To optimize the relevant factors that involve in reducing sugars production by

    ASKA reaction through two-level full factorial and central composite

    rotatable design (CCD).

    iv. To determine the end product of ASKA hydrolysis reaction using HPLC.

    1.4 Scopes of research

    i. Determination of the best substrate for ASKA using nine food-grade starches.

    ii. Possible reducing sugars production ranges determination using conventional

    one-factor-at-a-time (OFAT).

    iii. Optimization and validation of reducing sugars production by ASKA

    enzymatic reaction through 23 full factorial design and central composite

    design (CCD).

    iv. Analysis of ASKA reaction products by HPLC.

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